Methods for preparing 7alpha-hydroxy-dehydroepiandrosterone

ABSTRACT

The invention relates to new processes for preparing 7alpha-hydroxy-dehydroepiandrosterone of formula (1):

[0001] The invention relates to new processes for preparing 7alpha-hydroxy-dehydroepiandrosterone of formula (1):

[0002] 7alpha-Hydroxy-dehydroepiandrosterone (7α-OH-DHEA) is a derivative well known in the scientific literature; the following documents may be cited in particular:

[0003] FR-A1-2 771 105;

[0004] WO-A1-94/03176 and WO-A1-92/03925.

[0005] Each of the aforementioned documents reports a synthesis process for 7α-OH-DHEA. FR-A1-2 771 105 describes a process for preparing 7α-OH-DHEA in one step from dehydroepiandrosterone (DHEA), using a fungus: Fusarium moniliforme. This bioconversion process allows the direct transformation of DHEA into its 7-alpha-hydroxylated derivative with a yield of 79%.

[0006] This process allows the preparation of 7α-hydroxy-DHEA in a single step, but uses Fusarium moniliforme, which is a microscopic phytopathogenic fungus. This fungus attacks maize and sorghum (see in particular a document published on the internet at the following site: http://pested.unl.edu/catmans/fum.skp/fumchp8.htm). In addition, Fusarium moniliforme secretes oncogenic toxins which may prove highly dangerous to humans (see in particular a document published on the internet at the following site: http://www.hsafety.unc.edu/Manuals/LabManual/app7a.htm).

[0007] WO-A1-94/03176 and WO-A1-92/03925 describe a 4-step chemical process for preparing 7α-OH-DHEA from 3-O-acetyl-DHEA.

[0008] The first step of this process makes it possible to obtain 3-O-acetyl-7-bromo-DHEA from 3-O-acetyl-DHEA (commercial starting product) by treatment with a brominating agent. The mixture of 3-O-acetyl-7-bromo-DHEA isomers obtained is unstable and must be used quickly in the remainder of the process.

[0009] In a second step the racemic mixture of 7α-bromo and 7β-bromo isomers is equilibrated to give the 7α-bromo isomer (the more thermodynamically stable isomer) in majority form.

[0010] Following equilibration, the 3-O-acetyl-7-bromo-DHEA, treated with a mixture of glacial acetic acid and silver acetate, makes it possible to obtain 3-O-acetyl-7α-O-acetyl-DHEA.

[0011] 3-O-Acetyl-7α-O-acetyl-DHEA, treated with sodium carbonate (Na₂CO₃) in a mixture consisting of water and methanol, gives 7α-OH-DHEA, which is subsequently purified by crystallization.

[0012] This 4-step synthesis process has the prime disadvantage of necessitating a non-stereoselective bromination step (second step), which leads to unstable brominated intermediates. Furthermore, the process necessitates an equilibration step, permitting the thermodynamic isomer (7α-bromo-3-O-acetyl-DHEA) to be obtained predominantly. The equilibration step as described in WO-A1-94/03176 and WO-A1-92/03925 is ambiguous, since the relative proportion of the isomers 7α- and 7β-bromo-3-O-acetyl-DHEA obtained after equilibration is not specified.

[0013] It should also be noted that the process described does not report the yield obtained and does not specify the optical purity of the resultant 7α-OH-DHEA, this compound being documented solely by its melting point following recrystallization (192-193° C.).

[0014] Furthermore, the deacetalization conditions which are reported in the prior art do not allow satisfactory production of 7α-OH-DHEA from 3-O-acetyl-7α-OH-DHEA.

[0015] These conditions consist

[0016] either in a conventional method of saponification, using sodium hydroxide in an aqueous medium,

[0017] or in a method described in WO-A1-94/03176 and WO-A1-92/03925, which involves a reaction of double deacetalization of 3-O-acetyl-7-O-acetyl-DHEA by treatment with sodium carbonate in a mixture consisting of water and methanol.

[0018] These methods, applied to the reaction of deacetalization of 3-O-acetyl-7-O-acetyl-DHEA or of 3-O-acetyl-7α-OH-DHEA, lead to mixtures of products in which 7α-OH-DHEA occurs predominantly. This is because the reaction conditions used are not adapted and lead to the formation of decomposition products including in particular those obtained from the dehydration of the alcohol in position 7 of 3-O-acetyl-7α-OH-DHEA. There is therefore understandable interest in implementing processes which allow the preparation of 7α-OH-DHEA simply and rapidly, with industrially acceptable yields, with a diastereoselectivity which does not require a step of equilibration or of removal of the minority diastereoisomer (7β-OH), the processes having the advantage, moreover, of not involving phytopathogenic and/or oncogenic microorganisms.

[0019] Furthermore, the processes according to the present invention also have the advantage of including a deacetalization reaction which allows 7α-OH-DHEA to be obtained from 3-O-acetyl-7α-OH-DHEA under satisfactory conditions without the formation of decomposition products.

[0020] This is the aim of the present invention, whose objects include providing novel synthesis processes for DHEA.

[0021] The present invention provides a process for preparing 7α-OH-DHEA of formula (1) from 3-O-acetyl-7α-OH-DHEA of formula (4) according to a step (iii) consisting in a transesterification reaction using an alkali metal alkoxide in the corresponding alcohol.

[0022] The transesterification reaction which is used in the process of the invention consists essentially in

[0023] a) dissolving 3-O-acetyl-7α-OH-DHEA in an alcoholic solvent selected from ethanol, methanol and tert-butanol, preferably methanol;

[0024] b) adding between 1 and 3 equivalents, preferably between 1.5 and 3 equivalents, advantageously 1 equivalent of an alkali metal alkoxide, the alkoxide being selected preferably from the ethoxide, the tert-butoxide and the methoxide, advantageously the methoxide, and the alkali metal being selected preferably from lithium, sodium and potassium, advantageously sodium;

[0025] c) stirring the reaction mixture for a period of between 0.5 and 12 h, preferably between 1 h and 5 h, advantageously for 2 h;

[0026] d) evaporating the reaction solvent and diluting the mixture with water before extracting it with a solvent selected preferably from dichloromethane, ethyl acetate, chloroform and diethyl ether, advantageously dichloromethane;

[0027] e) drying the organic phase and then evaporating it to dryness;

[0028] f) optionally purifying the residue, for example by chromatography.

[0029] Advantageously the invention relates to a process for preparing 7α-OH-DHEA of formula (1) from 3-O-acetyl-7-oxo-DHEA of formula (3) comprising step (iii) as defined above, characterized in that step (iii) is preceded by a step (ii) comprising a regioselective and diastereoselective reduction of 3-O-acetyl-7-oxo-DHEA using L-Selectride® as reducing agent.

[0030] According to one preferred embodiment of the invention, the reduction of the enone of 3-O-acetyl-7-oxo-DHEA of formula (3) can be accomplished regio-selectively and diastereoselectively, without prior protection of the carbonyl in position 17, by using as reducing agent L-Selectride® or lithium tri-sec-butyl-borohydride (LiB[CH(CH₃)C₂H₅]₃H) in accordance with a method described in Steroids, 1998, 63, 454-458, which has been modified.

[0031] This method consists essentially in

[0032] a) preparing a solution of 3-O-acetyl-7-oxo-DHEA in an anhydrous organic polar solvent selected from tetrahydrofuran (THF), benzene and diethyl ether, preferably THF;

[0033] b) cooling the solution to a temperature of between −90 and −10° C., preferably between −80 and −60° C., advantageously to −78° C.;

[0034] c) adding under an inert atmosphere between 0.9 and 1.1 equivalents of L-Selectride®, preferably between 0.95 and 1.05 and, advantageously, 1 equivalent;

[0035] d) stirring the solution at a temperature of between −90 and −10° C., preferably between −80 and −60° C., advantageously at −78° C. for a period of between 1 and 10 h, preferably for 5 h;

[0036] e) taking the temperature of the reaction mixture to between −10 and 10° C., preferably to 0° C.;

[0037] f) adding aqueous sodium hydroxide (NaOH) solution, preferably at a concentration of between 1 and 10 M, advantageously 6 M, followed by aqueous hydrogen peroxide (H₂O₂) solution, preferably at 30 to 50%, advantageously at 30%, and stirring at ambient temperature;

[0038] g) diluting the reaction mixture in an organic polar solvent selected from diethyl ether, ethyl acetate, chloroform and dichloromethane, preferably diethyl ether;

[0039] h) washing the mixture a number of times by aqueous acidic washing, preferably with at least one aqueous 5% citric acid solution, then washing with at least one aqueous basic solution, preferably with saturated potassium bicarbonate (KHCO₃) solution, then washing with at least one aqueous neutral solution;

[0040] i) drying the organic phase and then evaporating it to dryness;

[0041] j) optionally purifying the residue, for example by chromatography.

[0042] Advantageously the invention relates to a process for preparing 7α-OH-DHEA of formula (1) from 3-O-acetyl-DHEA of formula (2) which comprises steps (iii) and (ii) as described above, characterized in that step (ii) is preceded by a step (i) consisting in a reaction of oxidation in the allyl position of 3-O-acetyl-DHEA.

[0043] FIG. 1 illustrates this 3-step synthesis process for 7α-OH-DHEA in accordance with the invention.

[0044] According to the invention a first preferred embodiment of the oxidation reaction in the allyl position of 3-O-acetyl-DHEA of formula (2) is carried out according to a method described in Tetrahedron Letters, 1997, 38, 119-122, which has been modified. This document describes a method of allylic oxidation by a peroxide in the presence of a copper salt catalyst on steroid frameworks.

[0045] This method consists essentially in

[0046] a) dissolving 3-O-acetyl-DHEA in an organic solvent or a mixture of organic solvents, selected preferably from acetonitrile, cyclohexane, benzene, methanol, ethanol and tert-butanol, advantageously acetonitrile;

[0047] b) adding under an inert atmosphere between 0.005 and 0.1 equivalent of copper, preferably 0.01 equivalent, preferably in the form of a copper salt, selected for example from copper iodide (CuI), copper bromide (CuBr), copper chloride (CuCl) and copper(II) chloride (CuCl₂), advantageously CuI;

[0048] c) cooling the reaction mixture at a temperature of between −10 and 10° C., advantageously between 5 and 10° C.;

[0049] d) adding dropwise between 5 and 10 equivalents, preferably 6 equivalents, of organic or inorganic peroxide, preferably organic peroxide, selected for example from alkyl hydroperoxide, advantageously t-butyl hydroperoxide (t-BuOOH);

[0050] e) allowing the temperature of the reaction mixture to rise to ambient temperature and stirring it for a period of between 0.5 and 4 h, preferably 2 h;

[0051] f) heating the mixture at a temperature of between 40 and 80° C., preferably between 50 and 70° C., advantageously at 50° C., for a period of between 4 and 72 h, preferably between 16 and 24 h, advantageously for 20 h;

[0052] g) cooling the reaction mixture and adding it to an aqueous alkaline solution, preferably 10% sodium bicarbonate (NaHCO₃) solution;

[0053] h) extracting the aqueous phase with an organic solvent, selected for example from diethyl ether, ethyl acetate, chloroform and dichloromethane, preferably diethyl ether, then washing the organic phases with an aqueous alkaline solution, preferably saturated aqueous NaHCO₃ solution, and optionally with saturated aqueous sodium chloride (NaCl) solution;

[0054] i) drying the organic phases and evaporating them to dryness under vacuum;

[0055] j) optionally purifying the residue in accordance with customary methods.

[0056] According to the invention a second preferred embodiment of the oxidation reaction in the allyl position of 3-O-acetyl-DHEA of formula (2) is carried out according to a method described in WO 92/03925 and WO 94/03176, which has been modified. These documents describe a method of allyl oxidation of 3-O-acetyl-DHEA by a mixture of acid anhydride, acetic acid and sodium acetate in the presence of chromium trioxide (CrO₃).

[0057] This method consists essentially in

[0058] a) preparing a mixture consisting of 3-O-acetyl-DHEA; acid anhydride, in an amount of preferably between 3 and 20 equivalents, advantageously 11 equivalents; acetic acid, in an amount of preferably between 20 and 120 equivalents, advantageously 66 equivalents; and sodium acetate, in an amount of preferably between 1 and 5 equivalents, advantageously 3 equivalents;

[0059] b) subjecting the reaction mixture to stirring and heating it to a temperature of between 40 and 60° C., preferably between 56 and 58° C.;

[0060] c) adding between 1 and 10 equivalents of an oxide, preferably between 2 and 6 equivalents, advantageously 3.5 equivalents, the oxide being selectable from an oxide of chromium, of manganese, of selenium and of magnesium, and being preferably an oxide of chromium, advantageously chromium trioxide (CrO₃);

[0061] d) keeping the reaction mixture under stirring for a period of between 0.5 and 4 h, preferably for 1 h, at a temperature of between 40 and 60° C., preferably between 56 and 58° C.;

[0062] e) cooling the reaction mixture and adding it, with stirring, to a solution consisting of water and ice;

[0063] f) filtering off the resulting precipitate and then washing it a number of times with water;

[0064] g) drying the residue and optionally purifying it in accordance with customary methods; preferably the product is recrystallized.

[0065] According to the invention a third preferred embodiment of the oxidation reaction in the allyl position of 3-O-acetyl-DHEA of formula (2) is carried out by a method described in WO 98/50409, which has been modified. This document describes a method of allyl oxidation using an alkali metal periodate and an alkyl hydroperoxide.

[0066] This method consists essentially in

[0067] a) dissolving 3-O-acetyl-DHEA of formula (2) in an organic solvent or an organic solvent mixture, selected preferably from acetone, heptane, acetonitrile, tert-butanol, pyridine, petroleum ether, hexane, isooctane and cyclohexane, advantageously in a mixture consisting of acetone and heptane, very preferably in a 1/1 ratio;

[0068] b) adding between 10 and 15 equivalents of alkyl hydroperoxide, advantageously t-butyl hydroperoxide, preferably at 70% or 80% in water;

[0069] c) stirring the mixture at ambient temperature and adding between 1 and 5 equivalents, preferably 3 equivalents, of alkali metal periodate, advantageously sodium periodate (NaIO₄);

[0070] d) adding water in an amount sufficient to allow total solubilization of the periodate in the reaction mixture, advantageously between 10% and 50% by volume, preferably between 15% and 40% by volume, very preferably between 20% and 30% by volume;

[0071] e) adding between 1 and 5 equivalents, preferably 3 equivalents, of an organic base, preferably pyridine, or a weak inorganic base, selected preferably from alkali metal carbonates and bicarbonates, advantageously sodium bicarbonate;

[0072] f) stirring the solution for a period of between 8 and 48 h, preferably for 14 h, at ambient temperature;

[0073] g) diluting the reaction mixture with ethyl acetate, dichloromethane, chloroform or diethyl ether, preferably ethyl acetate;

[0074] h) washing the mixture a number of times with aqueous sodium sulphate solution and then with water;

[0075] i) drying the organic phase and then evaporating it to dryness;

[0076] j) optionally purifying the residue in accordance with customary methods, preferably by recrystallization.

[0077] According to the invention an inert atmosphere means argon or nitrogen and ambient temperature means a temperature between 15 and 25° C. The purification methods which can optionally be employed at the end of each of the steps of the processes in accordance with the invention are realized according to conventional methods used in organic synthesis.

[0078] As mentioned above, the reaction of reduction of 3-O-acetyl-DHEA by L-Selectride® is diastereoselective: the diastereoisomer obtained selectively is 3-O-acetyl-7α-OH-DHEA. On the other hand the reaction of reduction of 3-O-acetyl-DHEA by L-Selectride® may give rise to a not insignificant amount of product reduced in positions 7 and 17. This secondary product can be easily removed, for example by chromatography, at this stage or after the transesterification reaction of step (iii).

[0079] However, in order to prevent the formation of the product reduced in positions 7 and 17 in step (ii), a process for preparing 7α-OH-DHEA in accordance with the present invention may further comprise additional steps of protection and then deprotection of the carbonyl in position 17 of the reacting species.

[0080] Thus the invention relates advantageously to a process for preparing 7alpha-hydroxy-dehydroepiandrosterone of formula (1) from 3-O-acetyl-dehydroepiandrosterone, comprising steps (i), (ii) and (iii) as described above, characterized in that it further comprises the following additional steps:

[0081] (iv) a reaction of protection of the carbonyl in position 17 of 3-O-acetyl-DHEA before step (i);

[0082] (v) a reaction of deprotection of the carbonyl in position 17 of the derivative obtained after step (ii), the said reaction of deprotection taking place before step (iii).

[0083] The protection of the carbonyl in position 17 of 3-O-acetyl-DHEA can be carried out in accordance with methods conventionally used in organic synthesis and well known to the person skilled in the art, such as, for example, those described in Protective Groups in Organic Synthesis, T. W. Greene, P. G. M. Wuts (Wiley Interscience).

[0084] According to the invention the carbonyl in position 17 of 3-O-acetyl-DHEA can be protected in cyclic or non-cyclic acetal form, in cyclic or non-cyclic dithioacetal form, in monothioacetal form, in O-substituted cyanohydrin form, in substituted hydrazone form, or in imine, enamine, imidazolidine or benzothiazole form. Advantageously the carbonyl in position 17 of 3-O-acetyl-DHEA can be protected in cyclic or non-cyclic acetal, cyclic or non-cyclic dithioacetal, imine, enamine or imidazolidine form.

[0085] According to the invention a first preferred embodiment of the protection of the carbonyl in position 17 of 3-O-acetyl-DHEA according to step (iv) can be carried out by protecting the carbonyl in position 17 in cyclic acetal form in accordance with a method described in Synth. Comm. 1995, 25, 395-404, which has been modified.

[0086] This method consists essentially in

[0087] a) preparing a solution consisting of 3-O-acetyl-DHEA of formula (2), a diol, preferably ethylene glycol, and an excess of desiccant, selected preferably from molecular sieve and ethyl orthoformate, preferably ethyl orthoformate, advantageously in a respective ratio of 1 mmol/3 ml/2 ml;

[0088] b) adding a catalytic amount of proton, the source thereof being advantageously para-toluenesulphonic acid or ion exchange resins;

[0089] c) stirring the mixture at a temperature of between 30 and 60° C., preferably at 40° C., for a period of between 1 and 8 h, preferably 3 h;

[0090] d) bringing the temperature of the reaction mixture to ambient temperature;

[0091] e) adding aqueous NaHCO₃ solution;

[0092] f) extracting the mixture with a solvent selected from dichloromethane, chloroform, ethyl acetate and diethyl ether, preferably with dichloromethane;

[0093] g) washing the organic phase, drying it and then evaporating it to dryness;

[0094] h) optionally purifying the residue in accordance with customary methods, preferably by chromatography on silica gel.

[0095] According to the invention a second preferred embodiment of the protection of the carbonyl in position 17 of 3-O-acetyl-DHEA according to step (iv) may be carried out by protecting the carbonyl in position 17 in cyclic acetal form in accordance with an azeotropic distillation method described in Synth. Comm. 1995, 25, 395-404, which has been modified.

[0096] This method consists essentially in

[0097] a) bringing to reflux a mixture consisting of 3-O-acetyl-DHEA of formula (2), ethylene glycol and para-toluenesulphonic acid (p-TsOH) in solution in benzene, preferably in a respective ratio of 1 mmol/5 ml/0.1 mmol/20 ml, in an assembly allowing azeotropic distillation to be conducted, preferably equipped with a Dean-Stark apparatus;

[0098] b) heating the mixture at a temperature of between 80 and 100° C., preferably at reflux of the benzene, for a period of between 4 and 48 h, preferably for 24 h;

[0099] c) allowing the temperature of the reaction mixture to return to ambient temperature;

[0100] d) drying the aqueous phase and then evaporating it to dryness;

[0101] e) optionally purifying the residue in accordance with customary methods, preferably by recrystallization.

[0102] The methods of deprotection of the carbonyl in position 17 of 3-O-acetyl-7α-hydroxy-DHEA protected in position 17 can be carried out in accordance with methods conventionally used in organic synthesis and well known to the person skilled in the art, such as, for example, those described in Protective Groups in Organic Synthesis, T. W. Greene, P. G. M. Wuts (Wiley Interscience).

[0103] Thus according to the invention a first preferred embodiment of the deprotection of the carbonyl in position 17 of 3-O-acetyl-7α-hydroxy-DHEA protected in position 17 in acetal form, preferably in cyclic acetal form, according to step (v) can be carried out in accordance with a method described in Steroids 1996, 61, 453-460, which has been modified.

[0104] This method consists essentially in

[0105] a) dissolving 3-O-acetyl-7α-hydroxy-DHEA protected in position 17 in acetal form in a mixture comprising water and a water-miscible solvent, preferably acetone, preferably in a 1/1 ratio by volume;

[0106] b) adding para-toluenesulphonic acid (p-TsOH), preferably 1 equivalent;

[0107] c) stirring the solution for a period of between 4 and 48 h, preferably 24 h, at ambient temperature;

[0108] d) evaporating the water-miscible solvent under vacuum;

[0109] e) diluting the reaction mixture with an organic solvent, selected preferably from ethyl acetate, dichloromethane, chloroform and diethyl ether, advantageously ethyl acetate, then washing it a number of times with water;

[0110] f) drying the organic phase and then evaporating it to dryness;

[0111] g) optionally purifying the residue in accordance with customary methods, preferably by recrystallization.

[0112] According to the invention a second preferred embodiment of the deprotection of the carbonyl in position 17 of the 3-O-acetyl-7α-hydroxy-DHEA protected in position 17 in acetal form, preferably cyclic acetal form, according to step (v) can be carried out in accordance with a method described in Steroids 1996, 61, 453-460, which has been modified.

[0113] Thus according to this other preferred embodiment of the invention the carbonyl in position 17 of the 3-O-acetyl-7α-hydroxy-DHEA protected in position 17 in acetal form, preferably in cyclic acetal form, is deprotected by a method described in Synth. Comm. 1995, 25, 395-404, which has been modified.

[0114] This method consists essentially in

[0115] a) preparing a solution consisting of 3-O-acetyl-7α-hydroxy-DHEA protected in position 17 in acetal form, preferably in cyclic acetal form, corresponding advantageously to 1,3-dioxolane or to 1,3-dioxane, in an organic solvent selected from benzene, chloroform and dichloromethane, preferably chloroform;

[0116] b) adding copper sulphate adsorbed on silica in an amount of between 2 and 4 g, preferably 2.5 g, per mmol of 3-O-acetyl-7α-hydroxy-DHEA protected in position 17 in acetal form;

[0117] c) stirring the reaction mixture for a period of between 1 to 48 h, preferably between 2 and 20 h, advantageously 6 h at a temperature of between 20 and 80° C., preferably between 50 and 70° C., advantageously at 60° C.;

[0118] d) filtering off the silica and concentrating the mixture to dryness;

[0119] e) optionally purifying the residue in accordance with customary methods, preferably by recrystallization.

[0120] The invention is illustrated in more detail in the following examples, which describe the various steps of the process in accordance with the invention.

EXAMPLE 1 Synthesis of 3-O-acetyl-7-oxo-DHEA of Formula (3)

[0121]

[0122] Method 1

[0123] A solution of 10 g of 3-O-acetyl-DHEA in 200 ml of acetonitrile is prepared. 60 mg of CuI are added under an inert atmosphere. The solution is cooled to between 5 and 10° C. and 19.6 ml of 80% t-BuOOH are added dropwise. At the end of the addition the temperature of the reaction mixture is allowed to rise to room temperature and it is stirred for 2 h and then heated at 50° C. for 20 h. The reaction mixture is subsequently cooled and is poured into 300 g of 10% sodium bicarbonate (NaHCO₃) solution. The mixture is extracted 3 times with diethyl ether and then the organic solution is washed with saturated NaHCO₃ solution and then with saturated sodium chloride (NaCl) solution. Drying and evaporation to dryness give the crude product in solid form. The residue is recrystallized from an acetone/hexane mixture.

[0124] Melting point: 190-192° C.;

[0125] yield: 91%;

[0126] [α]_(d)=−76° (methanol);

[0127]¹H NMR and mass spectrometry are in agreement.

[0128] Method 2

[0129] A solution is prepared consisting of a mixture of 6.5 ml of acetic anhydride (Ac₂O), 23 ml of acetic acid (AcOH), 1.7 g of sodium acetate (NaOAc) and 2 g of 3-O-acetyl-DHEA. This system is stirred and the reaction mixture is heated to between 56 and 58° C. Subsequently 2 g of chromium trioxide (CrO₃) are added over 30 minutes, while keeping the temperature constant at between 56-58° C. The solution is stirred at this temperature for 1 h after the end of the addition, then cooled and added slowly (while stirring) to a solution of 600 ml of ice-water. The precipitate is filtered off and washed with water until it no longer has a green colour. It is dried under vacuum with diphosphorus pentoxide (P₂O₅) and recrystallized from methanol to give the product of formula (3) in solid form.

[0130] Melting point: 191-192° C.;

[0131] yield: 50-70%.

EXAMPLE 2 Synthesis of 3-O-acetyl-7α-OH-DHEA of Formula (4)

[0132]

[0133] A solution of 300 mg of 3-O-acetyl-7-oxo-DHEA in 20 ml of anhydrous THF is prepared and is cooled to −78° C. 0.78 ml of L-Selectride®, sold by Aldrich (1 M in THF), is added dropwise under an inert atmosphere. The solution is stirred at −78° C. for 5 h. The reaction mixture is taken to 0° C. and 0.9 ml of NaOH solution (6 M) is added, followed by 0.9 ml of H₂O₂ (30%), and the mixture is stirred at ambient temperature for 30 minutes. It is diluted in 120 ml of diethyl ether. After a number of aqueous acid (5% citric acid), basic (saturated KHCO₃) and neutral washes, the organic solution is dried and then evaporated to dryness. The residue comprises 3-O-acetyl-7α-OH-DHEA (diastereoisomer obtained selectively) and approximately 10% of the product reduced in positions 7 and 17. The 7β-OH diastereoisomer was not identified in the mixture.

[0134] The residue is purified by chromatography to give 3-O-acetyl-7α-OH-DHEA in solid form.

[0135] Yield=70%;

[0136]¹H NMR and mass spectrometry are in agreement.

EXAMPLE 3 Synthesis of 7α-OH-DHEA of Formula (1)

[0137]

[0138] A solution of 3-O-acetyl-7α-OH-DHEA in methanol is prepared. 1 molar equivalent of sodium methoxide (NaOMe) is added and the mixture is stirred for a period of between 3 to 12 h. The methanol is evaporated, and the mixture is diluted with water and extracted with dichloromethane. The organic solution is dried then evaporated to dryness. The residue is purified by chromatography to give 7α-OH-DHEA in solid form.

[0139] Yield: 70%;

[0140] [α]_(d)=−66° (methanol);

[0141] melting point: 172-173° C.;

[0142]¹H NMR and mass spectrometry are in agreement.

EXAMPLE 4 Synthesis of 3-O-acetyl-17,17-ethylenedioxy-DHEA

[0143]

[0144] A solution of 1 mmol of 3-O-acetyl-DHEA in 3 ml of ethylene glycol and 2 ml of ethyl orthoformate is prepared. A catalytic amount of p-TsOH is added and the mixture is stirred at 40° C. for 3 h. It is cooled to ambient temperature and 10% NaHCO₃ solution is added. The mixture is extracted 3 times with dichloromethane and then the organic solution is washed with saturated NaCl solution. Drying and evaporation to dryness give the crude product in solid form. The residue is purified on silica gel (EtOAc/hexane, 17/83).

[0145] Yield: 77%;

[0146] melting point=135-137° C. (MeOH).

EXAMPLE 5 Synthesis of 3-O-acetyl-7-oxo-17,17-ethylenedioxy-DHEA

[0147]

[0148] A solution of 374 mg of 3-O-acetyl-17,17-ethylenedioxy-DHEA in 3.5 ml of acetone and 3.5 ml of heptane is prepared. 2 ml of t-butyl hydroperoxide (70% in water) are added and the mixture is stirred at ambient temperature for 15 minutes, after which NaIO₄ (650 mg), water (0.9 ml) and sodium bicarbonate (55 mg) are added. This solution is subsequently stirred at ambient temperature for 14 h. The reaction mixture is diluted with ethyl acetate (10 ml) and washed with water, then 2 times with aqueous 15% sodium sulphate solution, then with water. Evaporation of the solvent gives the crude product in solid form, which is recrystallized from methanol.

[0149] Yield: 67%;

[0150] melting point: 182-183° C. (MeOH).

EXAMPLE 6 Synthesis of 3-O-acetyl-7α-hydroxy-17,17-ethylenedioxy-DHEA

[0151]

[0152] A solution of 800 mg of 3-O-acetyl-7-oxo-17,17-ethylenedioxy-DHEA in 20 ml of anhydrous THF is prepared and is cooled to −78° C. 2 ml of L-Selectride® (1 M in THF) are added dropwise under an inert atmosphere. The solution is stirred at −78° C. for 5 h. The reaction mixture is brought to 0° C. and 0.9 ml of NaOH solution (6 M) is added, followed by 2.25 ml of H₂O₂ (30%), and the mixture is stirred at ambient temperature for 30 minutes. It is diluted in 120 ml of diethyl ether. After a number of acid (5% citric acid), basic (saturated KHCO₃) and neutral washes, the organic solution is dried and then evaporated to dryness. The residue obtained, in which the 7β-hydroxy diastereoisomer was not identified, is purified by chromatography to give 3-O-acetyl-7α-hydroxy-17,17-ethylenedioxy-DHEA in solid form, which is purified on silica gel (EtOAc/hexane: 35/65).

[0153] Yield=75%;

[0154] melting point: 170-171° C.

EXAMPLE 7 Synthesis of 3-O-acetyl-7α-OH-DHEA of Formula (4) (4)

[0155]

[0156] A solution of 1 mmol of 3-O-acetyl-7α-hydroxy-17,17-ethylenedioxy-DHEA in an acetone/water mixture (in a 1/1 ratio by volume) is prepared and p-TsOH (1 equivalent) is added. The solution is stirred at ambient temperature for 24 h. The acetone is then evaporated under vacuum. The reaction mixture is diluted with ethyl acetate and then washed a number of times with water. The organic phase is dried and then evaporated to dryness. The residue is purified by chromatography and recrystallized.

[0157] Yield: 95%;

[0158] melting point: 168-169° C. (acetone/hexane). 

1. Process for preparing 7alpha-hydroxy-dehydroepiandrosterone of formula (1) as follows:

from 3-O-acetyl-7α-OH-DHEA, characterized in that it comprises a step (iii) consisting in a transesterification reaction using an alkali metal alkoxide in the corresponding alcohol.
 2. Preparation process according to claim 1, characterized in that step (iii) consists essentially in the following steps: a) dissolving 3-O-acetyl-7α-OH-DHEA in an alcoholic solvent, b) adding between 1 and 3 equivalents of an alkali metal alkoxide, c) stirring the reaction mixture for a period of between 0.5 and 12 h, d) evaporating the reaction solvent, diluting the mixture with water and extracting it with a solvent selected from dichloromethane, ethyl acetate, chloroform and diethyl ether, e) drying the organic phase and evaporating it to dryness, f) optionally purifying the residue.
 3. Preparation process according to claim 2, characterized in that in step a) the alcoholic solvent is selected from ethanol, methanol and tert-butanol; in step b) between 1 and 1.5 equivalents, advantageously 1 equivalent, of alkali metal alkoxide are added; in step c) the reaction mixture is stirred for a period of between 1 h and 5 h, advantageously for 2 h; in step d) the solvent is dichloromethane.
 4. Preparation process according to either of claims 2 and 3, characterized in that in step b) the alkoxide is selected from the ethoxide, the tert-butoxide and the methoxide.
 5. Preparation process according to any one of claims 2 to 4, characterized in that in step b) the alkali metal is selected from lithium, sodium and potassium.
 6. Process for preparing 7α-OH-DHEA from 3-O-acetyl-7-oxo-DHEA comprising step (iii) as defined in accordance with any one of the preceding claims, characterized in that step (iii) is preceded by a step (ii) consisting in a regioselective and diastereoselective reduction of 3-O-acetyl-7-oxo-DHEA, using L-Selectride® as reducing agent.
 7. Preparation process according to the preceding claim, characterized in that step (ii) consists essentially in the following steps: a) dissolving 3-O-acetyl-7-oxo-DHEA in an anhydrous organic polar solvent, b) cooling the solution to a temperature of between −90 and −10° C., c) adding under an inert atmosphere between 0.9 and 1.1 equivalents of L-Selectride®, d) stirring the solution at a temperature of between −90 and −10° C. for a period of between 1 and 10 h, e) taking the temperature of the reaction mixture to between −10 and 10° C., f) adding aqueous NaOH solution and aqueous H₂O₂ solution and stirring at ambient temperature, g) diluting the reaction mixture with an organic polar solvent, h) washing the mixture a number of times with at least one aqueous acidic solution, at least one aqueous basic solution and at least one aqueous neutral solution, i) drying the organic phase and then evaporating it to dryness, j) optionally purifying the residue.
 8. Preparation process according to claim 7, characterized in that in step a) the anhydrous organic solvent is selected from tetrahydrofuran (THF), benzene and diethyl ether; in step b) the solution is cooled to a temperature of −78° C.; in step c) between 0.95 and 1.05 equivalents, advantageously 1 equivalent, of L-Selectride® are added; in step d) the solution is stirred at a temperature of between −80 and −60° C., advantageously −78° C., for a period of between 1 and 10 h, advantageously 5 h; in step e) the temperature of the reaction mixture is brought to 0° C.; in step g) the organic polar solvent is selected from diethyl ether, ethyl acetate, chloroform and dichloromethane; in step h) the diluted reaction mixture is washed a number of times with at least one aqueous 5% citric acid solution, at least one basic saturated aqueous KHCO₃ solution and at least one aqueous neutral solution.
 9. Process for preparing 7α-OH-DHEA from 3-O-acetyl-DHEA, comprising steps (iii) and (ii) as defined in accordance with any one of the preceding claims, characterized in that step (ii) is preceded by a step (i) which consists in a reaction of oxidation in the allyl position of 3-O-acetyl-DHEA.
 10. Preparation process according to the preceding claim, characterized in that step (i) consists essentially in the steps of a) dissolving 3-O-acetyl-DHEA in an organic solvent or a mixture of organic solvents, b) adding between 0.005 and 0.1 equivalent of copper, c) cooling the reaction mixture to a temperature of between −10 and 10° C., d) adding between 5 and 10 equivalents of organic or inorganic peroxide, e) allowing the temperature of the reaction mixture to return to ambient temperature and stirring it for a period of between 0.5 and 4 h, f) heating the mixture at a temperature of between 40 and 80° C. for a period of between 4 and 72 h, g) cooling the reaction mixture and adding it to an aqueous alkaline solution, h) extracting the aqueous phase with an organic solvent, i) washing the organic phases with an aqueous alkaline solution and then optionally with saturated aqueous NaCl solution, j) drying the organic phases and evaporating them to dryness under vacuum, k) optionally purifying the residue.
 11. Preparation process according to the preceding claim, characterized in that in step a) the organic solvent is selected from acetonitrile, cyclohexane, benzene, methanol, ethanol and tert-butanol; in step b) 0.01 equivalent of copper is added, advantageously in salt form; in step c) the reaction mixture is cooled to a temperature of between 5 and 10° C.; in step d) 6 equivalents of organic or inorganic peroxide are added, advantageously an organic peroxide; in step e) the reaction mixture is allowed to return to ambient temperature and is stirred for 2 h; in step f) the mixture is heated at a temperature of between 50 and 70° C., advantageously 50° C., for a period of between 16 and 24 h, advantageously 20 h; in step g) the aqueous alkaline solution is a 10% NaHCO₃ solution; in step h) the organic solvent is selected from diethyl ether, ethyl acetate, chloroform and dichloromethane; in step i) the aqueous alkaline solution is saturated NaHCO₃ solution.
 12. Preparation process according to the preceding claim, characterized in that in step b) the copper salt is selected from CuI, CuBr, CuCl and CuCl₂.
 13. Preparation process according to any one of claims 10 to 12, characterized in that in step d) the organic peroxide is selected from alkyl hydroperoxide, advantageously t-butyl hydroperoxide.
 14. Preparation process according to claim 9, characterized in that step (i) consists essentially in the steps of a) preparing a mixture consisting of acid anhydride, acetic acid, sodium acetate and 3-O-acetyl-DHEA, b) subjecting the reaction mixture to stirring and heating it to a temperature of between 40 and 60° C., c) adding between 1 and 10 equivalents of an oxide, d) maintaining the reaction mixture under stirring for a period of between 0.5 and 4 h at a temperature of between 40 and 60° C., e) cooling the reaction mixture and adding it to a solution consisting of water and ice, f) filtering off the resultant precipitate and washing it a number of times with water, g) drying the residue and optionally purifying it.
 15. Preparation process according to claim 14, characterized in that in step b) the reaction mixture is heated to a temperature of between 56 and 58° C.; in step c) between 2 and 6 equivalents of oxide, advantageously 3.5 equivalents, are added; in step d), the reaction mixture is maintained under stirring for a period of 1 h at a temperature of between 56 and 58° C.
 16. Preparation process according to either of claims 14 and 15, characterized in that in step c) the oxide is one selected from an oxide of chromium, of manganese, of selenium or of magnesium, advantageously chromium trioxide (CrO₃).
 17. Preparation process according to claim 9, characterized in that step (i) consists essentially in the steps of a) dissolving 3-O-acetyl-DHEA in an organic solvent or a mixture of organic solvents, b) adding between 10 and 15 equivalents of alkyl hydroperoxide, c) stirring the mixture at ambient temperature and adding between 1 and 5 equivalents of an alkali metal periodate, d) adding water in an amount sufficient to allow complete solubilization of the periodate in the reaction mixture, advantageously between 10% and 50% by volume, e) adding between 1 and 5 equivalents of organic bases or of weak inorganic bases, f) stirring the solution at ambient temperature for a period of between 8 and 48 h, g) diluting the reaction mixture with an organic solvent, h) washing the mixture a number of times with aqueous sodium sulphate solution and then with water, i) drying the organic phase and then evaporating it to dryness, j) optionally purifying the residue.
 18. Preparation process according to the preceding claim, characterized in that in step a) the organic solvent(s) is or are selected from acetone, heptane, acetonitrile, tert-butanol, pyridine, petroleum ether, hexane, isooctane and cyclohexane; in step b) the alkyl hydroperoxide is t-butyl hydroperoxide; in step c) 3 equivalents of an alkali metal periodate are added, advantageously sodium periodate (NaIO₄); in step d) between 20 and 30% of water by volume is added; in step e) 3 equivalents of organic bases, advantageously pyridine, or of weak inorganic bases, advantageously selected from alkali metal carbonates and bicarbonates, are added; in step f) the solution is stirred at ambient temperature for a period of 14 h; in step g) the organic solvent is selected from ethyl acetate, dichloromethane, chloroform and diethyl ether.
 19. Preparation process according to either of claims 17 and 18, characterized in that in step a) 3-O-acetyl-DHEA is dissolved in an organic solvent mixture consisting of acetone and heptane, advantageously in a 1/1 ratio.
 20. Preparation process according to claim 19, characterized in that in step e) the weak inorganic base is sodium bicarbonate.
 21. Process for preparing 7alpha-hydroxy-dehydroepiandrosterone according to any one of claims 9 to 21, characterized in that it further comprises the following additional steps: (iv) a reaction of protection of the carbonyl in position 17 of 3-O-acetyl-DHEA before step (i); (v) a reaction of deprotection of the carbonyl in position 17 of the derivative obtained after step (ii), the said reaction of deprotection taking place before step (iii).
 22. Preparation process according to the preceding claim, characterized in that in step (iv) the reaction of protection of the carbonyl in position 17 of 3-O-acetyl-DHEA consists in forming a group selected from a cyclic or non-cyclic acetal group, a cyclic or non-cyclic dithioacetal group, a monothioacetal group, an O-substituted cyanohydrin group, a substituted hydrazone group or an imine, an enamine, an imidazolidine or a benzothiazole group.
 23. Preparation process according to the preceding claim, characterized in that the carbonyl in position 17 of 3-O-acetyl-DHEA is protected in the form of a group selected from a cyclic or non-cyclic acetal, cyclic or non-cyclic dithioacetal, imine, enamine or imidazolidine group, advantageously a cyclic acetal group.
 24. Preparation process according to any one of claims 21 to 23, characterized in that the carbonyl in position 17 of 3-O-acetyl-DHEA is protected in the form of a cyclic acetal corresponding to 1,3-dioxolane or 1,3-dioxane.
 25. Preparation process according to any one of claims 21 to 24, characterized in that the reaction of protection of the carbonyl in position 17 of 3-O-acetyl-DHEA is an acetalization reaction consisting essentially in the steps of a) preparing a solution consisting of 3-O-acetyl-DHEA, a diol and a desiccant, b) adding a catalytic amount of proton, c) stirring the mixture at a temperature of between 30 and 60° C. for a period of between 1 and 8 h, d) taking the temperature of the reaction mixture to ambient temperature, e) adding aqueous NaHCO₃ solution, f) extracting the mixture with a solvent selected from dichloromethane, chloroform, ethyl acetate and diethyl ether, g) drying the organic phase and evaporating it to dryness, h) optionally purifying the residue.
 26. Preparation process according to the preceding claim, characterized in that in step a) the diol is ethylene glycol and the desiccant is selected from molecular sieve and ethyl orthoformate; in step b) the source of the catalytic amount of proton is para-toluenesulphonic acid or ion exchange resins; in step c) the mixture is stirred at a temperature of 40° C. for 3 h; in step f) the solvent is dichloromethane.
 27. Preparation process according to either of claims 25 and 26, characterized in that in step a) the 3-O-acetyl-DHEA, the diol and the desiccant are present in the solution in a respective ratio of 1 mmol/3 ml/2 ml.
 28. Preparation process according to any one of claims 21 to 23, characterized in that the reaction of protection of the carbonyl in position 17 of 3-O-acetyl-DHEA is an acetalization reaction consisting essentially in the steps of a) bringing to reflux a mixture consisting of 3-O-acetyl-DHEA, ethylene glycol and para-toluenesulphonic acid (p-TsOH) in solution in benzene, in an assembly allowing an azeotropic distillation to be carried out, b) heating the solution at a temperature of between 80 and 100° C. for a period of between 4 and 48 h, c) allowing the reaction mixture to return to ambient temperature, d) drying the organic phase and evaporating it to dryness; e) optionally purifying the residue.
 29. Preparation process according to the preceding claim, characterized in that in step a) 3-O-acetyl-DHEA, ethylene glycol, para-toluenesulphonic acid and benzene are present in the solution in a respective ratio of 1 mmol/5 ml/0.1 mmol/20 ml and the assembly allowing an azeotropic distillation to be carried out is equipped with a Dean-Stark apparatus; in step b) the solution is heated at the reflux of the benzene for 24 h.
 30. Preparation process according to claim 21, characterized in that the deprotection reaction of step (v) is a deacetalization reaction.
 31. Preparation process according to the preceding claim, characterized in that the reaction of deprotection of the carbonyl of 3-O-acetyl-7α-hydroxy-DHEA protected in position 17 in acetal form according to any one of the processes described in claims 22 to 29 consists essentially in the steps of a) dissolving 3-O-acetyl-7α-hydroxy-DHEA protected in position 17 in acetal form in a mixture comprising water and a water-miscible solvent, b) adding para-toluenesulphonic acid, c) stirring the solution at ambient temperature for a period of between 4 and 48 h, d) evaporating the water-miscible solvent under vacuum, e) diluting the reaction mixture with an organic solvent and then washing it a number of times with water, f) drying the organic phase and evaporating it to dryness, g) optionally purifying the residue.
 32. Preparation process according to the preceding claim, characterized in that in step a) the water and the water-miscible solvent, advantageously acetone, are in a 1/1 ratio by volume; in step b) 1 equivalent of para-toluenesulphonic acid is added; in step c) the solution is stirred for 24 h; in step e) the organic solvent is selected from ethyl acetate, dichloromethane, chloroform and diethyl ether.
 33. Preparation process according to claim 30, characterized in that the reaction of deprotection of the carbonyl of 3-O-acetyl-7α-hydroxy-DHEA protected in position 17 in acetal form according to any one of the processes described in claims 22 to 29 consists essentially in the steps of a) preparing a solution consisting of 3-O-acetyl-7α-hydroxy-DHEA protected in position 17 in acetal form in an organic solvent, b) adding copper sulphate adsorbed on silica in an amount of between 2 and 4 g per mmol of 3-O-acetyl-7α-hydroxy-DHEA protected in position 17 in acetal form, c) stirring the reaction mixture at a temperature of between 20 and 80° C. for a period of between 1 to 48 h, d) filtering off the silica and concentrating the mixture to dryness, e) optionally purifying the residue.
 34. Preparation process according to the preceding claim, characterized in that in step a) the organic solvent is selected from benzene, chloroform and dichloromethane; in step b) the copper sulphate adsorbed on silica is added in an amount equal to 2.5 g per mmol of 3-O-acetyl-7α-hydroxy-DHEA protected in position 17 in acetal form; in step c) the reaction mixture is stirred for a period of between 2 and 20 h, advantageously 6 h, and at a temperature of between 50 and 70° C., advantageously 60° C. 